CA2568460A1 - Process for the preparation of nitric esters of monohydric alchols - Google Patents
Process for the preparation of nitric esters of monohydric alchols Download PDFInfo
- Publication number
- CA2568460A1 CA2568460A1 CA002568460A CA2568460A CA2568460A1 CA 2568460 A1 CA2568460 A1 CA 2568460A1 CA 002568460 A CA002568460 A CA 002568460A CA 2568460 A CA2568460 A CA 2568460A CA 2568460 A1 CA2568460 A1 CA 2568460A1
- Authority
- CA
- Canada
- Prior art keywords
- reaction
- process according
- acid
- carried out
- nitric
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract 14
- 150000002148 esters Chemical class 0.000 title claims abstract 4
- 238000002360 preparation method Methods 0.000 title claims abstract 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract 12
- 238000006243 chemical reaction Methods 0.000 claims abstract 11
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract 5
- 150000001298 alcohols Chemical class 0.000 claims abstract 5
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract 3
- 239000000203 mixture Substances 0.000 claims abstract 3
- 239000002253 acid Substances 0.000 claims 7
- 229940032330 sulfuric acid Drugs 0.000 claims 5
- 239000011541 reaction mixture Substances 0.000 claims 2
- 150000007513 acids Chemical class 0.000 claims 1
- 239000003153 chemical reaction reagent Substances 0.000 claims 1
- 230000032050 esterification Effects 0.000 claims 1
- 238000005886 esterification reaction Methods 0.000 claims 1
- 230000000802 nitrating effect Effects 0.000 claims 1
- 238000005191 phase separation Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C201/00—Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
- C07C201/02—Preparation of esters of nitric acid
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C203/00—Esters of nitric or nitrous acid
- C07C203/02—Esters of nitric acid
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The present invention relates to a process for the preparation of nitric esters of mono-hydric alcohols wherein a monohydric alcohol or a mixture of monohydric alcohols is converted with nitric acid to the corresponding nitric esters under adiabatic reaction conditions in the presence of sulfuric acid.
Claims (12)
1. A process for the preparation of nitric esters of monohydric alcohols, wherein a monohydric alcohol or a mixture of monohydric alcohols is reacted with ni-tric acid in the presence of sulfuric acid under adiabatic reaction conditions.
2. The process according to claim 1, wherein the monohydric alcohol is selected from primary monohydric alcohols.
3. The process according to claim 1, wherein the reaction takes place within a temperature range of 10 to 80 °C.
4. The process according to claim 1, wherein the reaction is carried out continu-ously.
5. The process according to claim 1, wherein the reaction is carried out in a reac-tor and wherein the time of reaction is from 0.01 to 30 seconds.
6. The process according to claim 1, wherein the reaction is carried out in a tubu-lar reactor.
7. The process according to claim 1, wherein the overall mixing energy put into the reaction mixture amounts from 10 to 1000 J/l (Joule/liter).
8. The process according to claim 1, wherein the reaction mixture at the end of reaction is submitted to phase separation.
9. The process according to claim 1, wherein the mixing ratio of nitric acid to sul-furic acid in the starting mixed acid and the concentrations of the used acids in the nitrating acid is chosen in such a way that the weight ratio of sulfuric acid to water in the final spent acid is at least 2:1 and lies within the range of from 2:1 to 5:1.
10. The process according to claim 1, wherein the mixing ratio of nitric acid to sul-furic acid in the starting mixed acid is chosen in such a way that the final spent acid resulting after reaction has a residual content of at least 0.5 wt % of nitric acid.
11. The process according to claim 1, wherein the reaction is carried out in such a way that the adiabatic temperature rise, calculated as the difference between the temperatures at the beginning and the end of the reaction, amounts from 20 to 50 °C.
12. The process according to claim 1, wherein as esterification reagent an aqueous nitric acid/sulfuric acid mixture is used.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102005055794.5 | 2005-11-21 | ||
| DE102005055794 | 2005-11-21 | ||
| DE102005056974 | 2005-11-30 | ||
| DE102005057555.2 | 2005-11-30 | ||
| DE102005056974.9 | 2005-11-30 | ||
| DE102005057555A DE102005057555B3 (en) | 2005-11-21 | 2005-11-30 | Preparation of nitric acid esters of univalent alcohols comprises reacting the univalent alcohols or its mixture with nitric acid esters in the presence of sulfuric acid under adiabatic reaction condition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2568460A1 true CA2568460A1 (en) | 2007-05-21 |
| CA2568460C CA2568460C (en) | 2010-08-17 |
Family
ID=37845144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2568460A Expired - Fee Related CA2568460C (en) | 2005-11-21 | 2006-11-17 | Process for the preparation of nitric esters of monohydric alchols |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US7632960B2 (en) |
| EP (1) | EP1792891B1 (en) |
| JP (1) | JP4632138B2 (en) |
| KR (1) | KR100812622B1 (en) |
| CN (1) | CN100537514C (en) |
| AT (1) | ATE471310T1 (en) |
| BR (1) | BRPI0604926B1 (en) |
| CA (1) | CA2568460C (en) |
| DE (2) | DE102005057555B3 (en) |
| ES (1) | ES2347455T3 (en) |
| PL (1) | PL1792891T3 (en) |
| RS (1) | RS51432B (en) |
| RU (1) | RU2351583C2 (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010148049A2 (en) * | 2009-06-16 | 2010-12-23 | Draths Corporation | Preparation of trans, trans muconic acid and trans, trans muconates |
| RU2472771C1 (en) * | 2011-08-01 | 2013-01-20 | Федеральное Казенное Предприятие "Бийский Олеумный Завод" | Method of producing 2-ethylhexyl nitrate (versions) |
| RU2485092C1 (en) * | 2011-12-23 | 2013-06-20 | Закрытое акционерное общество "Научно-производственное предприятие "Алтайспецпродукт" | Method of producing nitroesters of monoatomic alcohols |
| DE102013110952B4 (en) | 2013-08-15 | 2015-11-26 | Josef Meissner Gmbh & Co. Kg | Process for the removal of impurities resulting from the production of aliphatic nitrate esters |
| CN113105333A (en) * | 2014-03-07 | 2021-07-13 | 康宁股份有限公司 | Continuous synthesis of isooctyl nitrate in a flow reactor |
| CN106220508B (en) * | 2016-07-06 | 2018-07-31 | 北京兴有化工有限责任公司 | It reduces the acidity of cetane number improver and removes organic and inorganic impurity method |
| RU2640953C2 (en) * | 2016-07-12 | 2018-01-18 | Федеральное Казенное Предприятие "Бийский Олеумный Завод" | Method for obtaining 2-ethylhexylnitrate |
| EP4139277A1 (en) * | 2020-04-22 | 2023-03-01 | DSM IP Assets B.V. | Process for the preparation of alpha,omega-alkanediol mononitrate |
| WO2025067714A1 (en) | 2023-09-28 | 2025-04-03 | Josef Meissner Gmbh & Co. Kg | Method and device for drying and/or purifying nitrate esters |
Family Cites Families (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2618650A (en) * | 1950-06-24 | 1952-11-18 | Ethyl Corp | Manufacture of amyl nitrate |
| US2734910A (en) * | 1952-08-02 | 1956-02-14 | Manufacture of propyl nitrate | |
| US2768964A (en) | 1953-05-27 | 1956-10-30 | Du Pont | Production of alkyl nitrates |
| CH540878A (en) * | 1970-06-30 | 1973-10-15 | Council Scient Ind Res | Process for the production of aliphatic nitrates |
| CA1034603A (en) | 1973-10-05 | 1978-07-11 | Maurice W. Hunt | Water washing of nitroaromatic compounds prior to catalytic reduction |
| US4021498A (en) * | 1975-12-09 | 1977-05-03 | American Cyanamid Company | Adiabatic process for nitration of nitratable aromatic compounds |
| US4091042A (en) * | 1977-08-19 | 1978-05-23 | American Cyanamid Company | Continuous adiabatic process for the mononitration of benzene |
| DE3463647D1 (en) * | 1983-06-24 | 1987-06-19 | Aeci Ltd | A process for the manufacture of nitric acid esters |
| US4496782A (en) * | 1983-07-08 | 1985-01-29 | Air Products And Chemicals, Inc. | Nitric acid recovery by the adiabatic nitration of nitroaromatics with fortified spent acid |
| US4479905A (en) * | 1983-09-19 | 1984-10-30 | Ethyl Corporation | Nitration process |
| US5162568A (en) * | 1983-11-21 | 1992-11-10 | E. I. Du Pont De Nemours And Company | Nitration of alkanols |
| SI0722434T1 (en) | 1993-10-06 | 1998-12-31 | Nicox S.A. | Nitric esters having anti-inflammatory and/or analgesic activity and process for their preparation |
| KR100557005B1 (en) * | 1996-06-04 | 2006-10-24 | 퀸즈 유니버시티 엣 킹스턴 | Nitrate esters and their use for nervous system disorders |
| RU2147577C1 (en) | 1998-12-18 | 2000-04-20 | Институт проблем химической физики РАН | Method of preparing n-(2-nitroxyethyl)nicotineamide |
| JP2001002626A (en) | 1999-04-19 | 2001-01-09 | Sankyo Co Ltd | Production of nitric ester |
| RU2235118C1 (en) * | 2002-11-14 | 2004-08-27 | Открытое акционерное общество "Ангарская нефтехимическая компания" | Cetane number-increasing additive and a method for preparation thereof |
| RU2259348C1 (en) * | 2004-02-04 | 2005-08-27 | ФГУП "Бийский олеумный завод" | Method for preparing 2-ethylhexyl nitrate by continuous method |
-
2005
- 2005-11-30 DE DE102005057555A patent/DE102005057555B3/en not_active Expired - Fee Related
-
2006
- 2006-11-09 AT AT06023304T patent/ATE471310T1/en active
- 2006-11-09 ES ES06023304T patent/ES2347455T3/en active Active
- 2006-11-09 DE DE502006007218T patent/DE502006007218D1/en active Active
- 2006-11-09 PL PL06023304T patent/PL1792891T3/en unknown
- 2006-11-09 RS RSP-2010/0400A patent/RS51432B/en unknown
- 2006-11-09 EP EP06023304A patent/EP1792891B1/en active Active
- 2006-11-17 CA CA2568460A patent/CA2568460C/en not_active Expired - Fee Related
- 2006-11-17 JP JP2006310874A patent/JP4632138B2/en not_active Expired - Fee Related
- 2006-11-20 RU RU2006140866/04A patent/RU2351583C2/en active
- 2006-11-20 KR KR1020060114644A patent/KR100812622B1/en not_active Expired - Fee Related
- 2006-11-20 CN CNB2006101719811A patent/CN100537514C/en not_active Expired - Fee Related
- 2006-11-20 US US11/601,975 patent/US7632960B2/en not_active Expired - Fee Related
- 2006-11-21 BR BRPI0604926A patent/BRPI0604926B1/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| RS51432B (en) | 2011-04-30 |
| CA2568460C (en) | 2010-08-17 |
| US20070129563A1 (en) | 2007-06-07 |
| CN100537514C (en) | 2009-09-09 |
| ES2347455T3 (en) | 2010-10-29 |
| BRPI0604926B1 (en) | 2015-12-22 |
| RU2351583C2 (en) | 2009-04-10 |
| DE502006007218D1 (en) | 2010-07-29 |
| KR100812622B1 (en) | 2008-03-13 |
| RU2006140866A (en) | 2008-06-10 |
| JP4632138B2 (en) | 2011-02-16 |
| ATE471310T1 (en) | 2010-07-15 |
| BRPI0604926A (en) | 2007-09-04 |
| JP2007137881A (en) | 2007-06-07 |
| PL1792891T3 (en) | 2010-11-30 |
| DE102005057555B3 (en) | 2007-05-16 |
| CN1978423A (en) | 2007-06-13 |
| KR20070053632A (en) | 2007-05-25 |
| US7632960B2 (en) | 2009-12-15 |
| EP1792891A1 (en) | 2007-06-06 |
| EP1792891B1 (en) | 2010-06-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Arzamendi et al. | Alkaline and alkaline-earth metals compounds as catalysts for the methanolysis of sunflower oil | |
| Zhou et al. | Phase distributions of alcohol, glycerol, and catalyst in the transesterification of soybean oil | |
| DK173416B1 (en) | Process for producing hydrogen-rich gas | |
| WO2009007234A1 (en) | New process for producing esters from vegetable oils and/or animal fats by using heterogeneous catalysts, particularly in the presence of free acidity and water | |
| CA2568460A1 (en) | Process for the preparation of nitric esters of monohydric alchols | |
| NO161899B (en) | TREATMENT TOOLS. | |
| Mendow et al. | Biodiesel production by two-stage transesterification with ethanol by washing with neutral water and water saturated with carbon dioxide | |
| US8754255B2 (en) | Process of preparation of glyoxylic acid aqueous solution | |
| CN102659088B (en) | Water-phase synthesis method of sodium azide | |
| CN104478715B (en) | The preparation method of compound | |
| RU2532663C1 (en) | Method of obtaining cetane-increasing additives to diesel fuel | |
| CN101544587A (en) | Preparation method of alpha, alpha'-bis(tert-butyl peroxy) diisopropylbenzene | |
| US2676983A (en) | Process for preparing monochlorodifluoro acetyl fluoride | |
| JP5438671B2 (en) | Method for isolating concentrated paraffin sulfonic acid | |
| CN105358513A (en) | Process for the preparation of 3-heptanol from a mixture comprising 2-ethylhexanal and 3-heptyl formate | |
| JP5868178B2 (en) | Method for producing methanol | |
| CN112624915A (en) | Method for preparing 2, 5-dihydroxyterephthalic acid (DHTA) | |
| RU2066294C1 (en) | Method for cleaning of cubic boron nitride from impurity of its hexagonal modification | |
| EP2935192A1 (en) | Process for the preparation of adipic acid | |
| JP7464280B2 (en) | A method for producing an ester compound based on an environmentally friendly and highly efficient esterification reaction using a salt ion exchange method and the compound | |
| JP6013589B2 (en) | Method of reacting glycerin for organic salt formation | |
| CN111153794A (en) | Method for synthesizing ethyl palmitate by using dodecyl trimethyl ammonium chloride-based eutectic solvent catalyst | |
| JP2010069377A (en) | Magnesium oxide catalyst, and manufacturing method for fatty acid ester and glycerine using the catalyst | |
| WO1999041228A1 (en) | Preparation of methacrylic acid, derivatives thereof or precursors thereto | |
| BRPI0711110B1 (en) | process of obtaining ethyl esters or biodiesel and glycerinated soap from ethyl alcohol and vegetable oils with controlled fatty acid acidity |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKLA | Lapsed |
Effective date: 20191118 |